Note : Les descriptions sont présentées dans la langue officielle dans laquelle elles ont été soumises.
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WO 2020/216619 PCT/EP2020/059989
Description
Extrusion cylinder with means for conducting cooling or
heating medium
The present invention relates to extrusion cylinders which can
be temperature-controlled in an effective manner, and
production methods for such extrusion cylinders.
In the field of extrusion, it is often necessary to control
the temperature of extrusion cylinders which are used for the
conducting and mixing of extrudate, in which the extruder worm
circulates the extrudate. In particular in rubber extrusion it
is advantageous to firstly pre-heat the extrusion cylinder in
order to bring the extrudate more quickly into a plastically
deformable state. In the further process, however, the heat
generated during the conducting/mixing of the extrudate must
be partially dissipated again. Usually, a cooling or
respectively heating means such as e.g. water or suchlike is
used here, which is conducted via ducts to the extrusion
cylinder and serves as a heat exchanger.
In order to configure the heat exchange in as effective manner
as possible, it is recommended to bring the heat exchanger
into direct contact with the cylinder body. For this,
currently peripheral bores through the cylinder are used. As
it is not possible, however, to execute such deep hole bores
for large bore depths with sufficient accuracy, the axial
length of cylinder bodies provided with peripheral bores is
limited. As extrusion cylinders typically have a greater
length than can be dealt with by means of peripheral bores, it
is necessary to assemble an extrusion cylinder from several
individual parts. This takes place by connection flanges at
the ends of the individual cylinder segments.
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In addition to the high manufacturing- and assembly costs of
this system of cylinder segments, further problems occur in
addition.
On the one hand, it is desirable to prevent pressure losses of
the temperature control medium due to deflections which are
too intensive in the temperature control channels. In the case
of the currently used bores, this can not be accomplished,
however. Rather, sudden deflections of 1800 often occur within
the connection flanges. Also, no closed routing is present
within the temperature control system. Rather, this is
segmented into several circuits with undirected flow. The
temperature control is hereby difficult to govern and control
and must be carried out under high pressure.
A further problem consists in that a distribution of different
temperature control zones, therefore the setting of different
temperatures along the extrusion cylinder, must be oriented to
the length of the individual cylinder segments. A free
creation and positioning of temperature zones is not possible.
Also for the mixing of extrudate with relatively high
viscosity, such as of rubber for instance, it is advantageous
to screw pins from the exterior into the interior of the
extrusion cylinder. These pins project into the extrudate and,
in interaction with the movement of the extruder worm, promote
the mixing and plasticizing of the extrudate. For an optimum
effect, these pins should be distributed as uniformly as
possible over the length of the extrusion cylinder. However,
if the latter is divided into several segments which are
connected by flanges, no pins can be inserted in the region of
the flanges. Hereby, the extrusion process can slow down or
even worsen.
The currently used temperature control systems for extrusion
cylinders therefore lead to a deficient flexibility with
regard to the temperature-controllability of the cylinders and
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with regard to the arrangement of pins in the cylinder which
are advantageous for the mixing of the extrudate. In addition,
the production of an extrusion cylinder made of several
segments provided with deep hole bores is prone to error and
is costly. Owing to the high pressure loss in the bores and
the undirected conducting of flow, the operation of such
temperature control systems is also expensive.
It is an object of the present invention to indicate an
extrusion cylinder by which at least a portion - preferably
all - of the above-mentioned problems are solved. In addition,
it is an object of the present invention to indicate a
production method for such an extrusion cylinder.
This problem is solved by the subject of the independent
claims.
An extrusion cylinder can have a cylinder body for
accommodating an extruder worm, which is characterized in that
an outer wall of the cylinder body has at least one depression
which can be covered and which in the covered state is
suitable for conducting a cooling or heating medium for
controlling the temperature of the cylinder body.
Instead of providing bores in the interior of the cylinder
body, depressions are therefore produced in the outer wall of
the cylinder body, for example by the milling of one or more
continuous grooves into the outer wall of the cylinder body.
These depressions must be dimensioned here in such a manner
that a cooling or heating medium which is able to be used for
the temperature control of the cylinder body, such as for
instance water or a similar heat-exchanging fluid, can flow
through the depression without excessive pressure loss, when
this depression is covered. The depression can have here an
approximately rectangular cross-section with a width and/or a
height of 0.5 to 6 cm, e.g. lcm, 3 cm or 5 cm. The cross-
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section can, however, also have any other shape with a similar
area.
The ducts for the temperature control medium can therefore be
produced in a simple manner on the exterior of the cylinder
body. Hereby, substantially all restrictions for the geometry
of the cooling path which are given through the use of bore
holes are eliminated. It is possible in particular to provide
far longer cylinder segments from the exterior with
depressions than is possible by means of bores. Hereby it is
possible to produce the entire extrusion cylinder from one
piece or from only a few segments. This permits the number of
pins provided for the mixing/plasticizing to be increased,
whereby the quality of the extrudate is increased.
In addition, with external production of the temperature
control ducts as depressions in the cylinder outer wall, the
course of the ducts can be substantially freely determined.
Thus, the depressions can run e.g. in a spiral shape around
the cylinder. Hereby, it is possible to produce clearly
defined flow paths for the cooling or heating medium, in which
only a small pressure drop occurs. This facilitates the
setting of the cylinder body to a particular temperature.
Although the above-mentioned advantages are already achieved
through just the provision of the coverable depression, the
extrusion cylinder can also have cover elements which are
connected with the outer wall of the cylinder body in such a
way that they cover the at least one depression. This permits
the cooling or heating medium to be conducted through the
depression. Preferably, the covering takes place by the
welding of sheet metal onto the upwardly open side of the
depression. The cylinder body, provided with the depressions,
can, however, also be inserted into a sleeve, e.g. a sheet-
metal sleeve, which e.g. owing to press fit, closes all the
depressions in a tight manner. Entries and exits for the
cooling or heating medium can then be opened in the sleeve.
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The at least one depression can have straight segments which
run parallel to a longitudinal axis of the cylinder body, and
curved segments which produce a connection between two ends,
lying in an adjacent manner, of precisely two straight
segments. Through the connection of straight elements and
curved elements, thereby a flow path can be defined without
branches.
The depression therefore runs as it were "in serpentine lines"
around the cylinder body. Proceeding from an inlet point for
the cooling or heating medium, the depression runs firstly in
axial direction. At the end if this straight segment a curved
segment adjoins, which leads the depression in circumferential
direction of the cylinder body in such a manner that no
pressure losses occur. The radius of the curved segments can
amount here to 1 to 6 cm, e.g. 2 cm, 3 cm, 4 cm or 5 cm. At
the end of the curved segment, a straight segment adjoins
again, which runs back in axial direction. This change of
curved and radial segments is continued up to an outlet of the
cooling or heating medium, preferably in such a manner that
the depression includes the entire circumference of the
cylinder body like a sleeve. In this way, a flow path can be
defined in a simple manner, which permits an optimum
temperature control of the cylinder body without excessive
pressure losses.
The straight segments can extend out from at least one edge
region of the cylinder body and a portion of the curved
segments can be arranged in the edge region of the cylinder
body. This permits e.g. the cooling or heating medium to be
fed in from the edge of the cylinder body. The width of the
edge region from the end of the cylinder body can amount to
e.g. a thirtieth, a twentieth, a tenth or a fifth of the total
length of the cylinder body.
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The extrusion cylinder can have, furthermore, at least one
connection flange which is mounted by means of press-fit onto
the edge region of the cylinder body in such a manner that it
covers at least the curved segments which are situated in the
edge region. The connection flange itself can therefore serve
as a cover element. Hereby, the material consumption can be
reduced. The connection flange here can be both a flange for
connecting several cylinder body segments, therefore also a
flange for connecting with an inlet or outlet of the extrudate
into the extrusion cylinder. The extrusion cylinder can
therefore be used both in a conventional manner as a segment
of a longer cylinder, therefore also as an individual
extrusion cylinder. The decision regarding the use or
respectively the length of the cylinder is, however, no longer
limited here by the technical circumstances, but rather only
by the requirements of the operator of the extrusion system
which contains the cylinder.
The connection flange can have ducts which make it possible to
conduct cooling or heating medium into the depression and out
from the depression. In this way, the feeding and discharging
of cooling or heating medium can be guaranteed in a simple
manner, without further components being necessary.
The straight segments can extend out from the edge region of
the cylinder body by a predetermined length which is smaller
than the length of the cylinder body. For example, the
straight segments can have only three quarters, two thirds,
half, one third or one quarter of the total length of the
cylinder body. The corresponding depression is then suitable
for controlling the temperature of this length region of the
cylinder body. Hereby, therefore, a flexible temperature
setting of the cylinder body can be achieved.
The straight segments can also not reach to the edge regions
of the cylinder body. This means that the depression runs e.g.
only in the central region of the cylinder body. The
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depression can also be e.g. a sixth, quarter, or third of the
total length of the cylinder body away from one or both ends
of the cylinder body. This allows a central part of the
cylinder body to be temperature-controlled separately. Hereby
also a flexible temperature setting can be achieved.
At least two connection sites for the directing in and out of
cooling or heating medium into the depression can be arranged
on the cylinder body. The feeding and discharging of cooling
or heating medium therefore does not have to take place via
the edge regions of the cylinder body, but rather can be
carried out basically everywhere on the cylinder body. It is
also possible e.g. to use as a connection site a bore of a
flange which is mounted on the end of the cylinder body, and
to arrange a further connection site of the same temperature
control medium duct on the cylinder body. This also permits a
more flexible temperature setting.
The outer wall of the cylinder body can have a plurality of
depressions which are not connected with one another and which
in the covered state define respectively their own flow path
for cooling or heating medium. This permits various, non-
communicating temperature control circuits to be provided,
which can set the cylinder body in their region to different
temperatures. Hereby also a more flexible temperature setting
is made possible.
The cylinder body can have a plurality of radial bore holes
which are suitable for receiving pins or screws. The bore
holes can be arranged at other locations than the at least one
depression. An extrusion cylinder which is able to be
temperature-controlled in a simple manner can in this way also
be occupied by pins, screws, bolts or suchlike which project
into the passage region for the extrudate and thus promote the
plasticizing and mixing of the extrudate. The boreholes which
are provided for this can be distributed over the entire
surface of the extrusion cylinder, so that a uniform action on
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the extrudate is made possible. If the boreholes do not
overlap with the depressions, i.e. the channels for the
cooling or heating medium, a simple interchanging of the pins
or screws sunken therein is possible without having to
interrupt the temperature control circuit. On the other hand,
it is also possible, after inserting of the screws, to close
the bore holes in a tight manner against the temperature
control medium so that, if necessary, they can also be
arranged in the region of the depression.
An extrusion device can have an extrusion cylinder, as was
described above, the at least one depression of which is
covered. In addition, the extrusion device can have cooling or
heating medium which runs in the at least one covered
depression. Hereby, the advantages which were explained above
are realized in operation of an extrusion device.
Furthermore, the extrusion device can have respectively a
temperature controlling arrangement for each depression, which
is suitable for controlling the temperature of the cooling or
heating medium running in the respective depression. Therefore
an extrusion with the use of an extrusion cylinder which is
able to be set to different temperature zones is possible.
A production method for an extrusion cylinder as was described
above can comprise: producing the at least one depression in
an outer wall of the cylinder body, for instance by milling.
The production method can furthermore comprise: covering the
at least one depression with a cover element, for instance
with sheet metal. This enables the simple production of the
extrusion cylinder by means of standard methods.
The present invention is described in detail below with
reference to the figures. This description is purely by way of
example. The invention itself is only determined by the
subject of the claims. There are shown:
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Fig. IA to IC various schematic views of an extrusion
cylinder;
Fig. 2A and 2B various schematic views of a further
extrusion cylinder;
Fig. 3 a schematic view of a further extrusion
cylinder;
Fig. 4A and 4B various views of further
extrusion
cylinders;
Fig. 5 a schematic view of a further extrusion
cylinder;
Fig. 6A and 6B schematic views of a further extrusion
cylinder;
Fig. 7 a schematic view of a further extrusion
cylinder; and
Fig. 8 a schematic flowchart for a production
method of an extrusion cylinder.
Fig. 1A to 1C show various schematic views of an extrusion
cylinder 100. Fig. 1A shows an oblique view, Fig. 1B a cross-
section through the extrusion cylinder 100 and Fig. 1C a side
view of the extrusion cylinder 100.
The extrusion cylinder 100 consists substantially of a
cylinder body 110, preferably manufactured from metal, which
is configured as a hollow cylinder. The cylinder body 110 has
an outer wall 115, which corresponds to the external covering
surface of the hollow cylinder. In the inside of the cylinder
body 110 an interior 118 exists, which serves to receive an
extruder worm and is suitable for the conducting, plasticizing
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and mixing of an extrudate, such as e.g. rubber, caoutchouc or
suchlike.
The dimensions of the extrusion cylinder 100 correspond here
to the dimensions usually used for extrusion and are
substantially dependent on the material which is to be
extruded. Typical dimensions for the total length of an
extrusion cylinder for rubber extrusion lie approximately in
the range of 1 to 5 metres and can therefore amount to e.g. 1
m, 2 m, 3 m, 4 m or 5 m. However, longer extrusion cylinders
are also conceivable.
The extrusion cylinder 100 can have a length which corresponds
to the entire length required for the extrusion. The extrusion
cylinder 100 can, however, also be a segment of the total
extrusion cylinder, which is then composed of several
extrusion cylinders. One or more of these cylinders can
correspond to the extrusion cylinder 100 or the modifications
of this cylinder which are discussed further below.
Typical dimensions for rubber extrusion for the outer radius
of the cylinder body 110 lie in the range of 20 to 50 cm, e.g.
25 cm, 30 cm, 35 cm, 40 cm or 45 cm. Possible inner radii lie
in the range of 4.5 cm to 30 cm, e.g. 5 cm, 10 cm, 15 cm, 20
cm or 25 cm. The wall thickness of the cylinder body 110
therefore lies in the range of 3 cm to 10 cm, e.g. 5 cm or 7
cm. A ratio of length to diameter can lie e.g. between 10:1
and 3:1, e.g. at ca. 4:1, 6:1, 7:1 or 8:1.
The cylinder body 110 has in its outer wall 115 at least one
depression 120. As shown in Fig. 1A to 1C, this can concern
here a single continuous depression 120, which runs around the
entire cylinder body 110. The depression 120 is configured
here, in particular with respect to its width and depth, in
such a manner that a cooling or heating medium, designated in
the following as temperature control medium, such as for
instance water or suchlike, can flow unimpeded, i.e. without
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excessive pressure loss, through the depression 120. In
addition, by the depression in the direction along the outer
wall 115 of the cylinder body 110 a flow path is to be
defined, which is as far as possible free of branches or
through the flow parameter of the temperature control medium -
and hence a heat exchange with the cylinder body 110 - can be
controlled or regulated in an uncomplicated manner, e.g.
through the placing of a valve or the conveying capacity of a
pump.
As shown in Fig. 1B, the depression 120 can have a depth for
this which corresponds to more than half of the wall thickness
of the cylinder body 110. The width of the depression can
correspond here to approximately its depth but can also differ
therefrom. For example, with a wall thickness of approximately
cm, the width of the depression 120 can lie in the range of
approximately 2 cm to 4 cm, e.g. at 3 cm. The depth of the
depression 120 then likewise lies in the range of 2 cm to 4
cm, e.g. likewise at 3 cm or at 3.5 cm. With another wall
thickness of the cylinder body 110, the said dimensions for
the depression 120 can either remain the same or be adapted
proportionally. Instead of the cross-section shape of the
depression 120 shown in Fig. 1B, this can also have any other
cross-section which is easy to produce, such as e.g. a
triangular shape or the shape of a circle segment, for
instance a semi-circular shape.
As shown in Fig. 1A and 1C, the depression 120 can be composed
of straight segments 122 and curved segments 124. The straight
segments 122 run here axially along the outer wall 115 of the
cylinder body 110. They can, as shown, extend out from an edge
region 112 of the cylinder body 110, e.g. up to the opposite
edge region. In the edge regions 112 the curved segments 124
are arranged. These connect respectively adjacent ends of
precisely two straight segments 122 with one another. As the
curved segments 124 are arranged respectively alternately in
the one or the other edge region 112, the depression 120 has a
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branch-free course. This means that a temperature control
medium can be conducted in a clearly defined manner from the
beginning of the depression 120 to its end.
In the region of the straight segments 122 a flow of the
temperature control medium is exposed to almost no resistance.
Here, substantially only the resistance due to the friction on
the walls of the depression 120 exists. The pressure loss
along the straight segments 122 is therefore relatively small.
The depression 120 is also configured in the edge regions 112
of the cylinder body 110 without abrupt transitions or edges.
Thereby, the flow resistance on transition between two
straight segments 122 remains low. As shown, the curved
segments 124 which are used for this can be configured as
circular arcs. The radii of the curved segments 124 are
selected in such a way that the flow resistance is minimized.
The radii can lie here in the range of 1 cm to 10 cm,
depending on the size of the cylinder body. For example, with
an external diameter of approximately 25 cm, radii of e.g. 1
cm, 1.5 cm or 2 cm can be used, whereas with an external
diameter of approximately 40 cm radii of 3 cm, 5 cm or 7 cm
are possible.
The course of the depression 120 shown in Fig. 1A to 1C (or in
the figures described further below) is to be regarded here as
purely by way of example. Basically any desired course forms
of the depression 120 are conceivable, such as e.g. a spiral-
shaped circulation with constant or varying spiral pitch. The
crucial factor for the shape or respectively the course of the
depression is solely that thereby an easy controlling or
respectively regulating of the temperature control of the
cylinder body 110 is possible and that pressure losses of a
temperature control medium flow are kept as small as possible.
This allows the cylinder body 110, and hence the extrusion
cylinder 100, to be able to be temperature-controlled in a
simple manner without excessive expenditure.
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The depression 120 can be introduced here in any suitable
manner for this into the outer wall 115 of the cylinder body
110. Preferably, the depression 120 is milled into the
cylinder body 110. This permits a particularly simple
production of the extrusion cylinder 100. The depression 120
can, however, also be produced differently, e.g. by means of
an etching method, by grinding, by a cast semi-finished
product including the depressions or suchlike.
The depression 120 of the extrusion cylinder 100, described
with reference to Fig. 1A to 1C, specifies the basic structure
for channels for the conducting of temperature control media.
In order to form these channels, as illustrated schematically
in Fig 2A, 2B and 3, cover elements 130 are connected with the
outer wall 115 of the cylinder body 110, through which the
depression 120 is closed in a tight manner. All the cover
elements 130 together only free inlet and outlets here which
are suitable for the introducing of the temperature control
medium into the depression 120.
As shown in Fig. 2A and 2B, in particular parts of the
depression which are not arranged within the edge regions 112
of the cylinder body 110 can be closed by cover elements 130
formed in the shape of the depression 120. In particular,
these segments of the depression 120 can be closed by metal
sheets which are brought into corresponding shape, e.g.
stamped, which are welded at the edges of the depression 120
with the cylinder body 110. However, other perfectly fitting
cover elements 130 are also conceivable, e.g. plastic
coverings. In addition, it is also possible to fasten the
cover elements 130 differently, e.g. by screwing, bonding or a
combination thereof. If necessary, sealing means can be
provided between cover elements 130 and the cylinder body 110,
in order to create tight channels for the temperature control
medium.
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As shown in Fig. 3, the segments of the depression, which are
arranged in edge regions 112 of the cylinder body 110, can be
covered by means of connection flanges 140, which are
connected e.g. by means of press-fit with the cylinder body
110. Through the press fit, the segments are closed in the
edge regions 112 in a tight manner. If, in addition, the cover
elements 130 in the centre region of the cylinder body 110
extend into the edge regions 112, a tight closure of the
depression 120 can be achieved without further sealing.
This is shown by way of example in Fig. 3, in which the
straight segments 122 of the depression 120, as shown in Fig.
2A, are closed by cover elements 130, e.g. welded-on metal
sheets, while the curved segments 124 are sealed by the
connection flanges 140 applied by mans of press fit. The
connection flanges 140 also overlap here a portion of the
straight segments 122. Hereby, in a simple manner a closure of
the depression 120 is achieved.
The connection flanges 140 can be configured here in such a
way that they enable a combination of several extrusion
cylinders 100 to a total cylinder. They can, however, also
represent the connection elements which serve for the
connecting of the extrusion cylinder 100 to the extrudate feed
and the output of the extrusion device, in which the extrusion
cylinder 100 is used.
Feeds and discharges can be arranged here at any desired
location on the cylinder body 110 or through the connection
flanges 140. For the feeding of the temperature control medium
in the central region of the cylinder body 110, a portion of
the depression 120 must remain unclosed for this, or
respectively the cover element 130 must be removed again at
this location or drilled out. This involves a certain effort,
but permits a simple and free positioning of feed points. With
feed via the connection flanges 140, these must have
corresponding bores which with the press fit come to lie over
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the desired free regions of the depression 120 in the edge
regions 112. When corresponding connection flanges 140 are
available, the feed of temperature control medium can thus be
produced without a further processing step.
Instead of the connection flanges 140 shown in Fig. 3, cover
elements 130, as are used in the central region of the
cylinder body 110, can also be used in the edge regions 112 of
the cylinder body 110 for closing the depression 120. The
closure then takes place in a uniform manner and is
independent of the use of connection flanges 140.
As shown in Fig. 4A and 4B, instead of the perfectly fitting
covering of the depression 120, a cover element 130 can also
be used which surrounds the entire cylinder body 110. For
example, a round metal sheet or a tube can be pushed by means
of press fit over the cylinder body 110, which then rests on
the cylinder body 110 in a tight manner in such a way that the
region of the depression 120 which is situated under the cover
element 130 is closed in a tight manner. As shown in Fig. 4B,
the cover element 130 can leave the edge regions 112 of the
cylinder body 110 free. These can, however, also be covered.
In Fig. 5 to 7 variants of the extrusion cylinder 100 are
shown, in which a plurality of depressions 120 is present. The
examples which are shown have respectively three depressions
120 which are not in connection. However, any number of
depressions 120 is possible. The depressions 120 surround a
respective region of the cylinder body 110 like a sleeve. They
therefore surround a portion of the cylinder body 110 with a
length which is smaller than the total length of the cylinder
body 110, entirely in circumferential direction of the
cylinder body 110. Through such depressions 120, which can
basically also be configured differently to that shown by way
of example in Fig. 5 to 7, various temperature control
circuits can be defined. Thereby, the extrusion cylinder 100
can be divided into various temperature zones, if this were to
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be necessary for the optimization of the extrusion process. In
particular, depressions 120 and hence temperature zones can be
produced, which do not lie in the edge regions 112 of the
cylinder body 110. It shall be understood that such a division
into various temperature zones can also take place in
circumferential direction. Then, a plurality of depressions
120 is necessary, in order to run around the cylinder body 110
in circumferential direction.
In an extrusion device which uses one of the extrusion
cylinders 100 described above, then to regulate the
temperature of each zone of the cylinder body 110 which is run
through by a depression 120 its own temperature control unit
can be provided. This enables the temperature to be set
entirely freely along the extrusion cylinder with
corresponding selection of the course of the depressions 120,
whereby the quality of the extrudate can be improved.
As shown in Fig. 5 to 7, the extrusion cylinder 100 can have a
plurality of connection sites 150, via which the temperature
control medium can be fed and discharged. These connection
sites 150 are positioned on the cylinder body 110 at the
beginning and at the end respectively of a depression 120. The
remaining regions of the depressions 120 are closed by means
of cover elements 130. As explained above, these can be
configured in a perfectly fitting manner (Fig. 5 and 7) or -
according to the variant described with reference to Fig. 4B -
as a sleeve completely surrounding the cylinder body 110 (Fig.
6A and 6B, the sleeve is shown here transparently, in order to
illustrate the depressions 120 lying therebeneath). In the
first case, the connection sites 150 can be simply applied,
e.g welded, screwed or bonded, onto regions of the depression
which remain free. In the second case, the cover elements 130
are opened at the desired sites and the connection sites 150
are then applied. With a termination of the extrusion cylinder
100 by means of connection flanges 140, as is shown in Fig. 7,
a portion of the feeding can also take place via the
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connection flanges 140. Through all these variants, a feed of
the temperature control medium which is flexible and tailored
to requirements is possible.
As shown in Fig. 3 and 7, the extrusion cylinder 100 can have
a plurality of boreholes 160, which entirely penetrate the
hollow cylinder, i.e. which produce a connection between the
interior 118 and the exterior of the cylinder body 110. Pins,
screws, bolts or suchlike can be inserted into such boreholes
160, which project into the interior 118 and there, during the
operation, improve the plasticizing and the mixing of the
extrudate as additional friction points. This takes place in
an effective manner with as uniform a distribution of the
boreholes 160 as possible.
Owing to the free distributability of the depressions 120,
which results from the simple production method of these
depressions 120, e.g. by milling, the boreholes 160 can also
be distributed uniformly over the cylinder body 110. In
addition, the production of the temperature control medium
channels from the exterior permits larger segments of the
total extrusion cylinder to be produced from one piece. With
corresponding configuration of the system which is used for
the production of the depression 120, extrusion cylinders 100
can also be manufactured which can be used as total extrusion
cylinders. This reduces the number of connection flanges
arranged on the length of the cylinder course. As no boreholes
160 can be arranged in the region of these flanges, through
the use of the extrusion cylinders 100 described above the
number of boreholes 160 and hence the number of pins promoting
the plasticizing and mixing of the extrudate can be increased
compared to conventional extrusion cylinders. The quality of
the extrudate is thereby improved.
Owing to the easier accessibility, the boreholes 160 are
preferably not formed in regions in which the depression 120
runs. However, it is also possible that depressions 120 and
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boreholes 160 overlap one another. With corresponding sealing
of the pins, inserted into the boreholes 160, against the
temperature control medium, this does not present a
fundamental problem. The boreholes 160 can therefore basically
be distributed entirely freely over the cylinder body 110.
Fig. 8 shows a schematic flowchart for a production method of
one of the extrusion cylinders described above. In a crucial
method step S810 for the production process, a depression is
introduced into the outer wall of an extrusion cylinder
suitable for the extrusion, in particular of rubber, which in
the covered state is suitable for the conducting of
temperature control medium. This preferably takes place by
milling the depression into the covering surface of a hollow
cylinder forming the extrusion cylinder. Optionally, at S820
subsequently the depression can be covered by means of cover
elements, preferably by welding-on or pressing-on of a metal
sheet.
In this way, temperature control medium channels for
controlling the temperature of the extrusion cylinder can be
introduced into the extrusion cylinder in a flexible, simple
and less error-prone manner. As the method is applied from the
exterior, it is possible to produce extrusion cylinders with
greater lengths than is known from the prior art. Hereby, the
production- and installation expenditure of extrusion devices
which use such extrusion cylinders is reduced. In addition, it
is possible to produce clearly defined flow channels for the
temperature control medium, which simplify and make more
flexible a temperature control of the extrusion cylinder.
Finally, owing to the increased length, the number of pins for
the plasticizing and mixing of extrudate which is conducted in
the extrusion cylinder can be increased, whereby the quality
of the extrudate can be improved.
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List of reference numbers
100 extrusion cylinder
110 cylinder body
112 edge region of the cylinder body
115 outer wall of the cylinder body
118 interior of the cylinder body
120 depression
122 straight segment of the depression
124 curved segment of the depression
130 cover element
140 connection flange
150 connection site
160 boreholes
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1
77438-WO 06.05.2021
PCT/EP2020/059989 Clean Version
Description
Extrusion cylinder with means for conducting cooling or
heating medium
The present invention relates to extrusion cylinders which can
be temperature-controlled in an effective manner, and production
methods for such extrusion cylinders.
In the field of extrusion, it is often necessary to control the
temperature of extrusion cylinders which are used for the
conducting and mixing of extrudate, in which the extruder worm
circulates the extrudate. In particular in rubber extrusion it
is advantageous to firstly pre-heat the extrusion cylinder in
order to bring the extrudate more quickly into a plastically
deformable state. In the further process, however, the heat
generated during the conducting/mixing of the extrudate must be
partially dissipated again. Usually, a cooling or respectively
heating means such as e.g. water or suchlike is used here, which
is conducted via ducts to the extrusion cylinder and serves as
a heat exchanger.
CN 208 745 314 U thus shows a cylinder cooling device for
extruders; US 2007 / 222 125 Al describes a plasticizing cylinder
with a plurality of heat tubes arranged within a pressure jacket,
which extend between a heating element and a cooling element.
JP H 05-57 768 discloses a production method for a composite
cylinder with a spiral jacket with temperature-regulating
output, wherein tube material is wound into a groove.
Further partial aspects are disclosed in SU 1 353 641 Al, CN 101
767 438 A, CN 2 915 484 Y, JP S56 173423 U, DE 40 13 538 Al and
JP H02 48319 U.
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In order to configure the heat exchange in as effective manner
as possible, it is recommended to bring the heat exchanger into
direct contact with the cylinder body. For this, currently
peripheral bores through the cylinder are used. As it is not
possible, however, to execute such deep hole bores for large
bore depths with sufficient accuracy, the axial length of
cylinder bodies provided with peripheral bores is limited. As
extrusion cylinders typically have a greater length than can be
dealt with by means of peripheral bores, it is necessary to
assemble an extrusion cylinder from several individual parts.
This takes place by connection flanges at the ends of the
individual cylinder segments.
In addition to the high manufacturing- and assembly costs of
this system of cylinder segments, further problems occur in
addition.
On the one hand, it is desirable to prevent pressure losses of
the temperature control medium due to deflections which are too
intensive in the temperature control channels. In the case of
the currently used bores, this can not be accomplished, however.
Rather, sudden deflections of 1800 often occur within the
connection flanges. Also, no closed routing is present within
the temperature control system. Rather, this is segmented into
several circuits with undirected flow. The temperature control
is hereby difficult to govern and control and must be carried
out under high pressure.
A further problem consists in that a distribution of different
temperature control zones, therefore the setting of different
temperatures along the extrusion cylinder, must be oriented to
the length of the individual cylinder segments. A free creation
and positioning of temperature zones is not possible.
Also for the mixing of extrudate with relatively high viscosity,
such as of rubber for instance, it is advantageous to screw pins
from the exterior into the interior of the extrusion cylinder.
These pins project into the extrudate and, in interaction with
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the movement of the extruder worm, promote the mixing and
plasticizing of the extrudate. For an optimum effect, these pins
should be distributed as uniformly as possible over the length
of the extrusion cylinder. However, if the latter is divided
into several segments which are connected by flanges, no pins
can be inserted in the region of the flanges. Hereby, the
extrusion process can slow down or even worsen.
The currently used temperature control systems for extrusion
cylinders therefore lead to a deficient flexibility with regard
to the temperature-controllability of the cylinders and with
regard to the arrangement of pins in the cylinder which are
advantageous for the mixing of the extrudate. In addition, the
production of an extrusion cylinder made of several segments
provided with deep hole bores is prone to error and is costly.
Owing to the high pressure loss in the bores and the undirected
conducting of flow, the operation of such temperature control
systems is also expensive.
It is an object of the present invention to indicate an extrusion
cylinder by which at least a portion - preferably all - of the
above-mentioned problems are solved. In addition, it is an
object of the present invention to indicate a production method
for such an extrusion cylinder.
This problem is solved by the subject of the independent claims.
An extrusion cylinder can have a cylinder body for accommodating
an extruder worm, which is characterized in that an outer wall
of the cylinder body has at least one depression which can be
covered and which in the covered state is suitable for conducting
a cooling or heating medium for controlling the temperature of
the cylinder body.
Instead of providing bores in the interior of the cylinder body,
depressions are therefore produced in the outer wall of the
cylinder body, for example by the milling of one or more
continuous grooves into the outer wall of the cylinder body.
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These depressions must be dimensioned here in such a manner that
a cooling or heating medium which is able to be used for the
temperature control of the cylinder body, such as for instance
water or a similar heat-exchanging fluid, can flow through the
depression without excessive pressure loss, when this depression
is covered. The depression can have here an approximately
rectangular cross-section with a width and/or a height of 0.5
to 6 cm, e.g. lcm, 3 cm or 5 cm. The cross-section can, however,
also have any other shape with a similar area.
The ducts for the temperature control medium can therefore be
produced in a simple manner on the exterior of the cylinder
body. Hereby, substantially all restrictions for the geometry
of the cooling path which are given through the use of bore
holes are eliminated. It is possible in particular to provide
far longer cylinder segments from the exterior with depressions
than is possible by means of bores. Hereby it is possible to
produce the entire extrusion cylinder from one piece or from
only a few segments. This permits the number of pins provided
for the mixing/plasticizing to be increased, whereby the quality
of the extrudate is increased.
In addition, with external production of the temperature control
ducts as depressions in the cylinder outer wall, the course of
the ducts can be substantially freely determined. Thus, the
depressions can run e.g. in a spiral shape around the cylinder.
Hereby, it is possible to produce clearly defined flow paths for
the cooling or heating medium, in which only a small pressure
drop occurs. This facilitates the setting of the cylinder body
to a particular temperature.
Although the above-mentioned advantages are already achieved
through just the provision of the coverable depression, the
extrusion cylinder also has cover elements which are connected
with the outer wall of the cylinder body in such a way that they
cover the at least one depression. This permits the cooling or
heating medium to be conducted through the depression.
Preferably, the covering takes place by the welding of sheet
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metal onto the upwardly open side of the depression. The cylinder
body, provided with the depressions, can, however, also be
inserted into a sleeve, e.g. a sheet-metal sleeve, which e.g.
owing to press fit, closes all the depressions in a tight manner.
Entries and exits for the cooling or heating medium can then be
opened in the sleeve.
The at least one depression has straight segments which run
parallel to a longitudinal axis of the cylinder body, and curved
segments which produce a connection between two ends, lying in
an adjacent manner, of precisely two straight segments. Through
the connection of straight segments and curved segments, thereby
a flow path can be defined without branches.
The depression therefore runs as it were "in serpentine lines"
around the cylinder body. Proceeding from an inlet point for the
cooling or heating medium, the depression runs firstly in axial
direction. At the end if this straight segment a curved segment
adjoins, which leads the depression in circumferential direction
of the cylinder body in such a manner that no pressure losses
occur. The radius of the curved segments can amount here to 1
to 6 cm, e.g. 2 am, 3 cm, 4 cm or 5 cm. At the end of the curved
segment, a straight segment adjoins again, which runs back in
axial direction. This change of curved and radial segments is
continued up to an outlet of the cooling or heating medium,
preferably in such a manner that the depression includes the
entire circumference of the cylinder body like a sleeve. In this
way, a flow path can be defined in a simple manner, which permits
an optimum temperature control of the cylinder body without
excessive pressure losses.
The straight segments can extend out from at least one edge
region of the cylinder body and a portion of the curved segments
can be arranged in the edge region of the cylinder body. This
permits e.g. the cooling or heating medium to be fed in from the
edge of the cylinder body. The width of the edge region from the
end of the cylinder body can amount to e.g. a thirtieth, a
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twentieth, a tenth or a fifth of the total length of the cylinder
body.
The extrusion cylinder can have, furthermore, at least one
connection flange which is mounted by means of press-fit onto
the edge region of the cylinder body in such a manner that it
covers at least the curved segments which are situated in the
edge region. The connection flange itself can therefore serve
as a cover element. Hereby, the material consumption can be
reduced. The connection flange here can be both a flange for
connecting several cylinder body segments, therefore also a
flange for connecting with an inlet or outlet of the extrudate
into the extrusion cylinder. The extrusion cylinder can
therefore be used both in a conventional manner as a segment of
a longer cylinder, therefore also as an individual extrusion
cylinder. The decision regarding the use or respectively the
length of the cylinder is, however, no longer limited here by
the technical circumstances, but rather only by the requirements
of the operator of the extrusion system which contains the
cylinder.
The connection flange can have ducts which make it possible to
conduct cooling or heating medium into the depression and out
from the depression. In this way, the feeding and discharging
of cooling or heating medium can be guaranteed in a simple
manner, without further components being necessary.
The straight segments can extend out from the edge region of the
cylinder body by a predetermined length which is smaller than
the length of the cylinder body. For example, the straight
segments can have only three quarters, two thirds, half, one
third or one quarter of the total length of the cylinder body.
The corresponding depression is then suitable for controlling
the temperature of this length region of the cylinder body.
Hereby, therefore, a flexible temperature setting of the
cylinder body can be achieved.
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The straight segments can also not reach to the edge regions of
the cylinder body. This means that the depression runs e.g. only
in the central region of the cylinder body. The depression can
also be e.g. a sixth, quarter, or third of the total length of
the cylinder body away from one or both ends of the cylinder
body. This allows a central part of the cylinder body to be
temperature-controlled separately. Hereby also a flexible
temperature setting can be achieved.
At least two connection sites for the directing in and out of
cooling or heating medium into the depression can be arranged
on the cylinder body. The feeding and discharging of cooling or
heating medium therefore does not have to take place via the
edge regions of the cylinder body, but rather can be carried out
basically everywhere on the cylinder body. It is also possible
e.g. to use as a connection site a bore of a flange which is
mounted on the end of the cylinder body, and to arrange a further
connection site of the same temperature control medium duct on
the cylinder body. This also permits a more flexible temperature
setting.
The outer wall of the cylinder body can have a plurality of
depressions which are not connected with one another and which
in the covered state define respectively their own flow path for
cooling or heating medium. This permits various, non-
communicating temperature control circuits to be provided, which
can set the cylinder body in their region to different
temperatures. Hereby also a more flexible temperature setting
is made possible.
The cylinder body can have a plurality of radial bore holes
which are suitable for receiving pins or screws. The bore holes
can be arranged at other locations than the at least one
depression. An extrusion cylinder which is able to be
temperature-controlled in a simple manner can in this way also
be occupied by pins, screws, bolts or suchlike which project
into the passage region for the extrudate and thus promote the
plasticizing and mixing of the extrudate. The boreholes which
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are provided for this can be distributed over the entire surface
of the extrusion cylinder, so that a uniform action on the
extrudate is made possible. If the boreholes do not overlap with
the depressions, i.e. the channels for the cooling or heating
medium, a simple interchanging of the pins or screws sunken
therein is possible without having to interrupt the temperature
control circuit. On the other hand, it is also possible, after
inserting of the screws, to close the bore holes in a tight
manner against the temperature control medium so that, if
necessary, they can also be arranged in the region of the
depression.
An extrusion device can have an extrusion cylinder, as was
described above, the at least one depression of which is covered.
In addition, the extrusion device can have cooling or heating
medium which runs in the at least one covered depression. Hereby,
the advantages which were explained above are realized in
operation of an extrusion device.
Furthermore, the extrusion device can have respectively a
temperature controlling arrangement for each depression, which
is suitable for controlling the temperature of the cooling or
heating medium running in the respective depression. Therefore
an extrusion with the use of an extrusion cylinder which is able
to be set to different temperature zones is possible.
A production method for an extrusion cylinder as was described
above can comprise: producing the at least one depression in an
outer wall of the cylinder body, for instance by milling. The
production method can furthermore comprise: covering the at
least one depression with a cover element, for instance with
sheet metal. This enables the simple production of the extrusion
cylinder by means of standard methods.
The present invention is described in detail below with
reference to the figures. This description is purely by way of
example. The invention itself is only determined by the subject
of the claims. There are shown:
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Fig. IA to IC various schematic views of an extrusion
cylinder;
Fig. 2A and 2B various schematic views of a further extrusion
cylinder;
Fig. 3 a schematic view of a further extrusion
cylinder;
Fig. 4A and 4B various views of further extrusion cylinders;
Fig. 5 a schematic view of a further extrusion
cylinder;
Fig. 6A and 6B schematic views of a further extrusion
cylinder;
Fig. 7 a schematic view of a further extrusion
cylinder; and
Fig. 8 a schematic flowchart for a production method
of an extrusion cylinder.
Fig. 1A to 1C show various schematic views of an extrusion
cylinder 100. Fig. 1A shows an oblique view, Fig. 1B a cross-
section through the extrusion cylinder 100 and Fig. 1C a side
view of the extrusion cylinder 100.
The extrusion cylinder 100 consists substantially of a cylinder
body 110, preferably manufactured from metal, which is
configured as a hollow cylinder. The cylinder body 110 has an
outer wall 115, which corresponds to the external covering
surface of the hollow cylinder. In the inside of the cylinder
body 110 an interior 118 exists, which serves to receive an
extruder worm and is suitable for the conducting, plasticizing
and mixing of an extrudate, such as e.g. rubber, caoutchouc or
suchlike.
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The dimensions of the extrusion cylinder 100 correspond here to
the dimensions usually used for extrusion and are substantially
dependent on the material which is to be extruded. Typical
dimensions for the total length of an extrusion cylinder for
rubber extrusion lie approximately in the range of 1 to 5 metres
and can therefore amount to e.g. 1 m, 2 m, 3 m, 4 m or 5 m.
However, longer extrusion cylinders are also conceivable.
The extrusion cylinder 100 can have a length which corresponds
to the entire length required for the extrusion. The extrusion
cylinder 100 can, however, also be a segment of the total
extrusion cylinder, which is then composed of several extrusion
cylinders. One or more of these cylinders can correspond to the
extrusion cylinder 100 or the modifications of this cylinder
which are discussed further below.
Typical dimensions for rubber extrusion for the outer radius of
the cylinder body 110 lie in the range of 20 to 50 cm, e.g. 25
cm, 30 cm, 35 cm, 40 cm or 45 cm. Possible inner radii lie in
the range of 4.5 cm to 30 cm, e.g. 5 cm, 10 cm, 15 cm, 20 cm or
25 cm. The wall thickness of the cylinder body 110 therefore
lies in the range of 3 cm to 10 cm, e.g. 5 cm or 7 cm. A ratio
of length to diameter can lie e.g. between 10:1 and 3:1, e.g.
at ca. 4:1, 6:1, 7:1 or 8:1.
The cylinder body 110 has in its outer wall 115 at least one
depression 120. As shown in Fig. 1A to 1C, this can concern here
a single continuous depression 120, which runs around the entire
cylinder body 110. The depression 120 is configured here, in
particular with respect to its width and depth, in such a manner
that a cooling or heating medium, designated in the following
as temperature control medium, such as for instance water or
suchlike, can flow unimpeded, i.e. without excessive pressure
loss, through the depression 120. In addition, by the depression
in the direction along the outer wall 115 of the cylinder body
110 a flow path is to be defined, which is as far as possible
free of branches or through the flow parameter of the temperature
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control medium - and hence a heat exchange with the cylinder
body 110 - can be controlled or regulated in an uncomplicated
manner, e.g. through the placing of a valve or the conveying
capacity of a pump.
As shown in Fig. 1B, the depression 120 can have a depth for
this which corresponds to more than half of the wall thickness
of the cylinder body 110. The width of the depression can
correspond here to approximately its depth but can also differ
therefrom. For example, with a wall thickness of approximately
cm, the width of the depression 120 can lie in the range of
approximately 2 cm to 4 cm, e.g. at 3 cm. The depth of the
depression 120 then likewise lies in the range of 2 cm to 4 cm,
e.g. likewise at 3 cm or at 3.5 cm. With another wall thickness
of the cylinder body 110, the said dimensions for the depression
120 can either remain the same or be adapted proportionally.
Instead of the cross-section shape of the depression 120 shown
in Fig. 1B, this can also have any other cross-section which is
easy to produce, such as e.g. a triangular shape or the shape
of a circle segment, for instance a semi-circular shape.
As shown in Fig. 1A and 1C, the depression 120 can be composed
of straight segments 122 and curved segments 124. The straight
segments 122 run here axially along the outer wall 115 of the
cylinder body 110. They can, as shown, extend out from an edge
region 112 of the cylinder body 110, e.g. up to the opposite
edge region. In the edge regions 112 the curved segments 124 are
arranged. These connect respectively adjacent ends of precisely
two straight segments 122 with one another. As the curved
segments 124 are arranged respectively alternately in the one
or the other edge region 112, the depression 120 has a branch-
free course. This means that a temperature control medium can
be conducted in a clearly defined manner from the beginning of
the depression 120 to its end.
In the region of the straight segments 122 a flow of the
temperature control medium is exposed to almost no resistance.
Here, substantially only the resistance due to the friction on
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the walls of the depression 120 exists. The pressure loss along
the straight segments 122 is therefore relatively small.
The depression 120 is also configured in the edge regions 112
of the cylinder body 110 without abrupt transitions or edges.
Thereby, the flow resistance on transition between two straight
segments 122 remains low. As shown, the curved segments 124
which are used for this can be configured as circular arcs. The
radii of the curved segments 124 are selected in such a way that
the flow resistance is minimized. The radii can lie here in the
range of 1 cm to 10 cm, depending on the size of the cylinder
body. For example, with an external diameter of approximately
25 cm, radii of e.g. 1 cm, 1.5 cm or 2 cm can be used, whereas
with an external diameter of approximately 40 cm radii of 3 cm,
cm or 7 cm are possible.
The course of the depression 120 shown in Fig. 1A to 1C (or in
the figures described further below) is to be regarded here as
purely by way of example. Basically any desired course forms of
the depression 120 are conceivable, such as e.g. a spiral-shaped
circulation with constant or varying spiral pitch. The crucial
factor for the shape or respectively the course of the depression
is solely that thereby an easy controlling or respectively
regulating of the temperature control of the cylinder body 110
is possible and that pressure losses of a temperature control
medium flow are kept as small as possible. This allows the
cylinder body 110, and hence the extrusion cylinder 100, to be
able to be temperature-controlled in a simple manner without
excessive expenditure.
The depression 120 can be introduced here in any suitable manner
for this into the outer wall 115 of the cylinder body 110.
Preferably, the depression 120 is milled into the cylinder body
110. This permits a particularly simple production of the
extrusion cylinder 100. The depression 120 can, however, also
be produced differently, e.g. by means of an etching method, by
grinding, by a cast semi-finished product including the
depressions or suchlike.
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The depression 120 of the extrusion cylinder 100, described with
reference to Fig. 1A to 1C, specifies the basic structure for
channels for the conducting of temperature control media. In
order to form these channels, as illustrated schematically in
Fig 2A, 2B and 3, cover elements 130 are connected with the
outer wall 115 of the cylinder body 110, through which the
depression 120 is closed in a tight manner. All the cover
elements 130 together only free inlet and outlets here which are
suitable for the introducing of the temperature control medium
into the depression 120.
As shown in Fig. 2A and 2B, in particular parts of the depression
which are not arranged within the edge regions 112 of the
cylinder body 110 can be closed by cover elements 130 formed in
the shape of the depression 120. In particular, these segments
of the depression 120 can be closed by metal sheets which are
brought into corresponding shape, e.g. stamped, which are welded
at the edges of the depression 120 with the cylinder body 110.
However, other perfectly fitting cover elements 130 are also
conceivable, e.g. plastic coverings. In addition, it is also
possible to fasten the cover elements 130 differently, e.g. by
screwing, bonding or a combination thereof. If necessary,
sealing means can be provided between cover elements 130 and the
cylinder body 110, in order to create tight channels for the
temperature control medium.
As shown in Fig. 3, the segments of the depression, which are
arranged in edge regions 112 of the cylinder body 110, can be
covered by means of connection flanges 140, which are connected
e.g. by means of press-fit with the cylinder body 110. Through
the press fit, the segments are closed in the edge regions 112
in a tight manner. If, in addition, the cover elements 130 in
the centre region of the cylinder body 110 extend into the edge
regions 112, a tight closure of the depression 120 can be
achieved without further sealing.
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This is shown by way of example in Fig. 3, in which the straight
segments 122 of the depression 120, as shown in Fig. 2A, are
closed by cover elements 130, e.g. welded-on metal sheets, while
the curved segments 124 are sealed by the connection flanges 140
applied by mans of press fit. The connection flanges 140 also
overlap here a portion of the straight segments 122. Hereby, in
a simple manner a closure of the depression 120 is achieved.
The connection flanges 140 can be configured here in such a way
that they enable a combination of several extrusion cylinders
100 to a total cylinder. They can, however, also represent the
connection elements which serve for the connecting of the
extrusion cylinder 100 to the extrudate feed and the output of
the extrusion device, in which the extrusion cylinder 100 is
used.
Feeds and discharges can be arranged here at any desired location
on the cylinder body 110 or through the connection flanges 140.
For the feeding of the temperature control medium in the central
region of the cylinder body 110, a portion of the depression 120
must remain unclosed for this, or respectively the cover element
130 must be removed again at this location or drilled out. This
involves a certain effort, but permits a simple and free
positioning of feed points. With feed via the connection flanges
140, these must have corresponding bores which with the press
fit come to lie over the desired free regions of the depression
120 in the edge regions 112. When corresponding connection
flanges 140 are available, the feed of temperature control
medium can thus be produced without a further processing step.
Instead of the connection flanges 140 shown in Fig. 3, cover
elements 130, as are used in the central region of the cylinder
body 110, can also be used in the edge regions 112 of the
cylinder body 110 for closing the depression 120. The closure
then takes place in a uniform manner and is independent of the
use of connection flanges 140.
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As shown in Fig. 4A and 4B, instead of the perfectly fitting
covering of the depression 120, a cover element 130 can also be
used which surrounds the entire cylinder body 110. For example,
a round metal sheet or a tube can be pushed by means of press
fit over the cylinder body 110, which then rests on the cylinder
body 110 in a tight manner in such a way that the region of the
depression 120 which is situated under the cover element 130 is
closed in a tight manner. As shown in Fig. 4B, the cover element
130 can leave the edge regions 112 of the cylinder body 110
free. These can, however, also be covered.
In Fig. 5 to 7 variants of the extrusion cylinder 100 are shown,
in which a plurality of depressions 120 is present. The examples
which are shown have respectively three depressions 120 which
are not in connection. However, any number of depressions 120
is possible. The depressions 120 surround a respective region
of the cylinder body 110 like a sleeve. They therefore surround
a portion of the cylinder body 110 with a length which is smaller
than the total length of the cylinder body 110, entirely in
circumferential direction of the cylinder body 110. Through such
depressions 120, which can basically also be configured
differently to that shown by way of example in Fig. 5 to 7,
various temperature control circuits can be defined. Thereby,
the extrusion cylinder 100 can be divided into various
temperature zones, if this were to be necessary for the
optimization of the extrusion process. In particular,
depressions 120 and hence temperature zones can be produced,
which do not lie in the edge regions 112 of the cylinder body
110. It shall be understood that such a division into various
temperature zones can also take place in circumferential
direction. Then, a plurality of depressions 120 is necessary,
in order to run around the cylinder body 110 in circumferential
direction.
In an extrusion device which uses one of the extrusion cylinders
100 described above, then to regulate the temperature of each
zone of the cylinder body 110 which is run through by a
depression 120 its own temperature control unit can be provided.
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This enables the temperature to be set entirely freely along the
extrusion cylinder with corresponding selection of the course
of the depressions 120, whereby the quality of the extrudate can
be improved.
As shown in Fig. 5 to 7, the extrusion cylinder 100 can have a
plurality of connection sites 150, via which the temperature
control medium can be fed and discharged. These connection sites
150 are positioned on the cylinder body 110 at the beginning and
at the end respectively of a depression 120. The remaining
regions of the depressions 120 are closed by means of cover
elements 130. As explained above, these can be configured in a
perfectly fitting manner (Fig. 5 and 7) or - according to the
variant described with reference to Fig. 4B - as a sleeve
completely surrounding the cylinder body 110 (Fig. 6A and 6B,
the sleeve is shown here transparently, in order to illustrate
the depressions 120 lying therebeneath). In the first case, the
connection sites 150 can be simply applied, e.g welded, screwed
or bonded, onto regions of the depression which remain free. In
the second case, the cover elements 130 are opened at the desired
sites and the connection sites 150 are then applied. With a
termination of the extrusion cylinder 100 by means of connection
flanges 140, as is shown in Fig. 7, a portion of the feeding can
also take place via the connection flanges 140. Through all
these variants, a feed of the temperature control medium which
is flexible and tailored to requirements is possible.
As shown in Fig. 3 and 7, the extrusion cylinder 100 can have a
plurality of boreholes 160, which entirely penetrate the hollow
cylinder, i.e. which produce a connection between the interior
118 and the exterior of the cylinder body 110. Pins, screws,
bolts or suchlike can be inserted into such boreholes 160, which
project into the interior 118 and there, during the operation,
improve the plasticizing and the mixing of the extrudate as
additional friction points. This takes place in an effective
manner with as uniform a distribution of the boreholes 160 as
possible.
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Owing to the free distributability of the depressions 120, which
results from the simple production method of these depressions
120, e.g. by milling, the boreholes 160 can also be distributed
uniformly over the cylinder body 110. In addition, the
production of the temperature control medium channels from the
exterior permits larger segments of the total extrusion cylinder
to be produced from one piece. With corresponding configuration
of the system which is used for the production of the depression
120, extrusion cylinders 100 can also be manufactured which can
be used as total extrusion cylinders. This reduces the number
of connection flanges arranged on the length of the cylinder
course. As no boreholes 160 can be arranged in the region of
these flanges, through the use of the extrusion cylinders 100
described above the number of boreholes 160 and hence the number
of pins promoting the plasticizing and mixing of the extrudate
can be increased compared to conventional extrusion cylinders.
The quality of the extrudate is thereby improved.
Owing to the easier accessibility, the boreholes 160 are
preferably not formed in regions in which the depression 120
runs. However, it is also possible that depressions 120 and
boreholes 160 overlap one another. With corresponding sealing
of the pins, inserted into the boreholes 160, against the
temperature control medium, this does not present a fundamental
problem. The boreholes 160 can therefore basically be
distributed entirely freely over the cylinder body 110.
Fig. 8 shows a schematic flowchart for a production method of
one of the extrusion cylinders described above. In a crucial
method step S810 for the production process, a depression is
introduced into the outer wall of an extrusion cylinder suitable
for the extrusion, in particular of rubber, which in the covered
state is suitable for the conducting of temperature control
medium. This preferably takes place by milling the depression
into the covering surface of a hollow cylinder forming the
extrusion cylinder. Optionally, at S820 subsequently the
depression can be covered by means of cover elements, preferably
by welding-on or pressing-on of a metal sheet.
AMENDED SHEET
Date Recue/Date Received 2021-09-16
CA 03133885 2021-09-16
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In this way, temperature control medium channels for controlling
the temperature of the extrusion cylinder can be introduced into
the extrusion cylinder in a flexible, simple and less error-
prone manner. As the method is applied from the exterior, it is
possible to produce extrusion cylinders with greater lengths
than is known from the prior art. Hereby, the production- and
installation expenditure of extrusion devices which use such
extrusion cylinders is reduced. In addition, it is possible to
produce clearly defined flow channels for the temperature
control medium, which simplify and make more flexible a
temperature control of the extrusion cylinder. Finally, owing
to the increased length, the number of pins for the plasticizing
and mixing of extrudate which is conducted in the extrusion
cylinder can be increased, whereby the quality of the extrudate
can be improved.
AMENDED SHEET
Date Recue/Date Received 2021-09-16
CA 03133885 2021-09-16
19
List of reference numbers
100 extrusion cylinder
110 cylinder body
112 edge region of the cylinder body
115 outer wall of the cylinder body
118 interior of the cylinder body
120 depression
122 straight segment of the depression
124 curved segment of the depression
130 cover element
140 connection flange
150 connection site
160 boreholes
AMENDED SHEET
Date Recue/Date Received 2021-09-16
